Composition and improved pH driven method for wastewater separation using an amphoteric carboxylate and a cationic destabilizer composition

ABSTRACT

Improved separation of emulsified hydrophobic organic soils can be obtained from aqueous effluents using an amphoteric carboxylate surfactant material in combination with cationic destabilizer or flocculent materials. Such a treatment in combination with an acidic pH adjustment causes the rapid separation of hydrophobic organic soils from the aqueous stream. The treated aqueous stream is environmentally compatible. 
     Improved laundry detergents comprising an organic amphoteric carboxylate surfactant and selected nonionic surfactants provide both cleaning for fiber and fabric containing items soiled with substantial quantities of hydrophobic soil. The pH of an effluent generated in such cleaning processes can be adjusted to an acid pH and treated with a cationic material causing a break that permits rapid and substantially complete separation of the hydrophobic organic soils from the effluent. Residual concentrations of organic soil in effluent water can be less than 250 ppm and can be as low as 10 ppm.

This is a continuation of application Ser. No. 08/429,896, filed Apr. 27, 1995, now abandoned which is a continuation of application Ser. No. 08/267,664, filed Jun. 29, 1994, now U.S. Pat. No. 5,523,000.

FIELD OF THE INVENTION

The invention relates to separating an emulsified hydrophobic organic soil from an aqueous effluent stream using a combination of an amphoteric carboxylate and a cationic coagulant, flocculent or destabilizer material, at an acidic pH. The amphoteric and the destabilizer material can be added together or separately and can be added at any point. Preferably the amphoteric is added in a detergent and the destabilizer materials are added after the organic soil is emulsified in the aqueous stream. Such contaminated aqueous effluent commonly arises in a number of institutional and industrial installations. These contaminated aqueous waste streams cannot be directly discarded in municipal waste treatment systems. Such waste streams can be treated with materials that can cause the hydrophobic organic soil to separate from the aqueous streams in a number of chemical addition protocols. The invention also relates to an improved cleaning composition for a fiber containing non-woven or woven fabric item contaminated with substantial quantities of organic hydrophobic soils such as fats, oils and greases and to methods for separating such soils from the cleaning process effluent. The cleaning method comprises an active chemical addition and contains a pH change step prior to disposal of the effluent, that causes the rapid separation of hydrophobic organic soils from effluent or wastewater. The cleaning composition can contain both organic and inorganic materials that cooperate to obtain cleaning and rapid hydrophobic soil separation from effluent.

BACKGROUND OF THE INVENTION

A number of institutional and industrial operations produce aqueous effluent contaminated with substantial proportions of hydrophobic organic soils. Such soils are commonly found in the waste stream as emulsified droplets dispersed in the waste stream. Such emulsions are commonly stabilized by the presence of one or more surfactants that are part of the effluent material. Commonly, nonionic surfactants act as stabilizing agents. Such waste streams are most commonly a result of the disposal of hydrophobic waste or a result of a cleaning operation wherein large quantities of hydrophobic soils are cleaned from environmental surfaces, clothing, rags, dishes and pans, etc. and other hydrophobic soil containing objects. The resulting aqueous effluent can contain substantial proportions of hydrophobic organic soils typically derived from fat, oil and grease. Prior to disposal, the aqueous effluent must be treated to separate such soils before the effluent can be safely discharged into municipal sewer systems.

The use of alkaline cleaning compositions containing inorganic detergent and builder components in combination with organic surfactant compositions and other components have been common for many years in laundry operations. Typical laundry processes involve contacting soiled woven or non-woven fabric with an aqueous cleaning composition containing proportions of laundry chemicals dissolved or suspended in the aqueous medium. The organic and inorganic chemicals cooperate to remove soil from fabric. The soils become suspended by the cleaning chemicals in the aqueous stream through the action of the active chemical cleaners.

In commercial laundry operations soil load and soil type can create substantial operating difficulties. A substantial proportion of the laundry workload will constitute items contaminated with such hydrophobic organic soil. Such items include mechanics' clothing, shop wipes, shop towels, contaminated uniforms, drop cloths, machine covers, mop heads, and other units typically manufactured from either synthetic or natural fibers woven or otherwise assembled into typically flexible units that can be soaked or saturated with substantial quantities of the hydrophobic organic soils. The hydrophobic organic soils typically involved in the cleaning methods and compositions of this invention comprise fats, oils and grease. Fats are typically organic materials derived from natural sources such as animals and plants. Fats are typically liquid or solid fatty acid glycerol esters, phospholipids, etc. and are typically produced in food processing but also have a number of industrial uses. Oils are commonly liquids produced from petroleum refining but can also include materials such as liquid vegetable oil, silicone oil, etc. Greases are commonly considered to be a heavy, thick solid or semisolid hydrocarbon or suspensions of organic or inorganic solid particulate materials in a fat or oil base. Greases are typically substantially semisolid or solid materials used in lubrication purposes. Commonly such hydrophobic organic soils are generated in kitchen, bar or other food service environments, in shop environments such as printing shops, metal working shops, auto repair shops, fast food outlets, restaurants, etc. In the operations of such installations, substantial quantities of fats, oils and greases are used and can come in contact with walls and floors of the installation and the clothing worn by employees. The environment of the installations are commonly cleaned using mops, shop towels, bar towels, bar mops, kitchen rags, wipes, rags and other cleaning instruments. The soil load can be as much as 20 wt-% , typically 5 wt-% to 17 wt-%, on the fabric.

Municipal, county, state and federal regulations often place stringent requirements on the concentration of a variety of contaminants in effluent. After laundering soiled items, the substantial quantity of organic soils in laundry effluent is often unacceptable environmentally due to the presence of up to 2000 ppm hydrophobic soil and often more. In the production of effluent from commercial laundries, fats, oils and greases are often required to be substantially less than 250 ppm and often between 10 and 100 ppm as measured by EPA analytical method 180.1.

Efficient laundry chemicals in aqueous media remove hydrophobic soils by creating an emulsion of the soil in the aqueous medium. The emulsion comprises small hydrophobic droplets sometimes called micelles which are surrounded and stabilized by the detergent or surfactant materials. The dispersed nature of the soil in aqueous medium is a substantial barrier to its removal after laundering. Before removal can be obtained, the micelle must be destabilized, the emulsion must be broken, the fats, oils and greases must be reassembled into a single phase and the single phase hydrophobic material must be separated from the aqueous solution. A number of methods for separating fats, oils and greases from laundry effluent have been attempted. One useful alternative involves changing the pH of the wash medium from neutral or mildly alkaline to acid to break the emulsion of the organic hydrophobic soil. Once the emulsion is broken, a separate phase of hydrophobic soil forms which can be readily removed.

Boettner et al., U.S. Pat. No. 3,117,999, teach a tertiary carbonimine substituted with both ethylene oxide and propylene oxide blocks to form nonionic surfactant materials. Dupre et al., U.S. Pat. No. 3,118,000, teach alkylamine compositions substituted with both ethylene oxide and propylene oxide blocks to produce nonionic surfactant material. Maloney et al., U.S. Pat. No. 4,605,773, teach a low foaming pH sensitive alkyl amine polyether surfactant that can be used in production of paper from recycled secondary fiber. The disclosed surfactants are pH sensitive and have substantial surfactant properties. Cohen, U.S. Pat. No. 5,110,503, teaches compositions and methods for cleaning hydrophobic organic soil containing contaminated fabric with methods of separating the hydrophobic soil from laundry effluent. Cohen uses a composition of matter comprising a first component, comprising a reaction product of an α,β-unsaturated acid and a short chain amine such as a β-amino dipropionic acid, having an assigned structure as RN(CH₂ CH₂ CO₂ H)₂, with a variety of ether surfactants such as an ethoxylate- propoxylate block copolymer, sulfates or sulfonates, alkoxylated phosphates. Lastly, McFarlan et al., U.S. Pat. No. 5,207,922, is primarily directed to a method of treating laundry effluent or wastewater for the purpose of separating fats, oils and greases. At Column 3, lines 19-60, McFarlan et al. teach typical laundry chemical compositions.

The comparative ability for separating hydrophobic organic soils such as fats, oils and greases from laundry effluent is typically characterized by the concentration of the chemicals used in the laundry, the pH at which the phase separation occurs, the rate of the phase separation and the final concentration in the aqueous effluent of hydrophobic soil such as residual fats, oils and greases. The degree of separation is pH sensitive. Reducing the pH as low as 2 can cause a clean break, however, such a low pH requires substantial amounts of acid and also exposes operating equipment and personnel to unacceptably low pH. Further, even at such low pH's some compositions fail to reach an acceptable level of fats, oils and greases in effluent. We have found in our work with pH sensitive laundry chemical systems that many such prior art systems have an unacceptably low pH requirement to obtain a clean separation or fail to reduce the concentration of fats, oils and greases in the aqueous effluent to a level sufficient to satisfy environmental regulations.

A substantial need continues to exist for a method of reducing the residual concentration of hydrophobic soils in aqueous waste streams using a pH change in a chemical addition protocol. Further, a need exists to improve laundry chemical systems that can be used in cleaning processes involving items having a substantial loading of hydrophobic organic soil in laundry effluent. Systems are needed that produce an effluent that can be treated after laundering to separate fats, oils and greases such that the final concentration in the aqueous effluent is less than 250 ppm and preferably substantially below 100 ppm.

BRIEF DESCRIPTION OF THE INVENTION

We have found that emulsified hydrophobic organic soil in an aqueous effluent stream can be separated using the combined action of a cationic destabilizer material and an amphoteric surfactant as set forth below. In a preferred mode, a laundry effluent or other effluent of a cleaning process containing an amphoteric carboxylate from the laundry detergent can be treated with a cationic coagulant or destabilizing material, at low pH, to cause the soil to separate from the aqueous stream. These materials in combination with a pH change cause a rapid demulsification, and a rapid separation of the hydrophobic soils from the aqueous stream. Within a short period of time the emulsion breaks, and a phase separation occurs when the hydrophobic soils separate from the aqueous medium leaving a low residual concentration of soil. The cationic materials and the amphoteric carboxylate surfactant can be added in a number of different modes at various stages of wastewater generation and transfer to discharge outlets including a single addition, portion-wise addition and continuous addition.

We have also found an alkaline cleaning composition useful in the processes of the invention comprising an effective detergent amount of a source of alkalinity, an effective amount of an amphoteric carboxylate surfactant of the formula: ##STR1## wherein X is a linear or branched alkylene, hydroxyalkylene or alkoxyalkylene group having 1-4 carbon atoms;

R is R⁴ --CO--NH in which R⁴ is a saturated or unsaturated, branched or linear alkyl group having 6-22 carbon atoms, or R⁴ ;

R¹ is hydrogen, A or (A)_(n) --X--CO₂ ⁻ Z⁺ in which A is a linear or branched alkyl, hydroxyalkyl or alkoxyalkyl having 1-4 carbon atoms, n is an integer from 0 to 6, and Z is an alkali metal cation, a hydrogen ion or an ammonium cation;

R² is (A)_(n) --X--CO₂ ⁻ Z⁺ ; and

R³ is absent or A; or, preferably, where R⁴ is alkyl as defined above having 9-17 carbon atoms, X is a linear alkyl group having 1-3 carbon atoms, n is 0-3, and Z is an alkali metal or ammonium cation, for example, the alkyl amino (mono and di)-acetates or propionates and amido (mono and di)-acetates or propionates and the betaine and dihydroglycinates of the above formula; and a nonionic surfactant composition comprising either a C₈₋₁₈ alcohol ethoxylate having 3 to 15 moles of ethylene oxide or a C₈₋₉ alkyl phenol ethoxylate having 4 to 15 moles of ethylene oxide per mole of surfactant. The detergent can be used with a flocculent or destabilizer to initiate a separation of organic hydrophobic soils from laundry effluents by a pH adjustment. The effective pH range is between 2 and 7, and is preferably between 3 and 6.5. Further, once the effective pH is reached and the separation occurs, the concentration of hydrophobic organic soils in the effluent can be as little as 100 ppm or lower. In our experimental work with the systems of this invention, we have found that the materials achieve a separation in a maximum concentration of hydrophobic organic soils in the effluent that is substantially and surprisingly better than the performance of prior art laundry chemicals when comparable amounts of chemicals are used.

DETAILED DESCRIPTION OF THE INVENTION

Emulsified hydrophobic soils can be effectively separated from aqueous streams using a combination of a cationic coagulant or destabilizer material and an amphoteric carboxylate surfactant. In a preferred laundry process, the amphoteric carboxylate is added in the laundry detergent. Adjusting the pH of the effluent followed by an addition of the cationic destabilizer causes a rapid demulsification of the aqueous stream, a rapid phase separation of the hydrophobic organic soil from the aqueous material which can then be readily separated. The amphoteric surfactant can be added at any stage in the production of the contaminated stream (e.g.) in a laundry chemical system, metered into a downstream pipe or conduit, or post added with the cationic destabilizer. The cationic destabilizer is typically added after the pH adjustment. The resulting treated aqueous stream containing minimal residual amounts of hydrophobic soil can then be discarded into a municipal waste treatment system.

The separation methods of the invention use a cationic destabilizer with an amphoteric carboxylate in a pH change protocol to separate soil. The laundry compositions of the invention include an effective concentration for detergent purposes of a source of alkalinity, a nonionic surfactant, and an amphoteric carboxylate containing surfactant to clean contaminated objects and surfaces.

The Cationic Flocculent or Destabilizer

In the compositions and methods of the invention, a flocculent or cationic destabilizer is added after a pH adjustment to acidic conditions. The flocculent causes the small emulsified particles to form large removable droplets or a separate phase of hydrophobic material. The cationic materials are a well known class of monomeric or polymeric chemicals that are used in separating liquid and solid soil phases from aqueous streams. Such cationic materials are disclosed in Polvelectrolytes for water and waste water treatment, Schwoyer, W.L.K. (CRC Press, Boca Raton, FL 1981). Generally, the cationic materials are inorganic or organic and are monomeric, oligomeric or polymeric.

Inorganic cationic materials include polyaluminum chloride aluminum sulfate or other alum materials such as ammonia alum or ammonium alum, potassium alums; calcium chloride, ferric chloride, ferric sulfate, ferrous sulfate, sodium aluminate, sodium silicate having an excess of sodium oxide over silicon dioxide, etc. Polyaluminum chloride is a polyaluminum oxide compound with a proportion of the oxide atoms substituted by chlorine atoms.

Organic cationic materials or cationic polyelectrolytes are typically prepared using common free radical addition polymerization, condensation reactions, an epoxide addition reaction and a variety of other reactions in existing polymer backbones including Hofmann degradation, Mannich reaction, and nucleophilic displacements. High molecular weight polymerized cationic materials are manufactured by polymerizing a cationic monomer. Cationic monomers include acrylic monomers such as tertiary nitrogen containing acrylates, tertiary nitrogen containing acrylamides, quaternary nitrogen containing acrylates and quaternary nitrogen containing acrylamides; heterocycloaromatic cyclic vinyl monomers such as vinylimidazolines, vinylpyridines, vinylbenzyl quaternary ammonium salts and allylamines.

Examples of the cationic acrylic monomer of the general formula are quaternary ammonium salts (using quaternizing agents such as methyl chloride, dimethyl sulfate, and benzyl chloride) of dialkylaminoalkyl (meth)acrylates such as dimethylaminoethyl (meth)acrylate, diethylaminoethyl (meth)acrylate, 3-dimethylamino-2-hydroxypropyl (meth)acrylate! and dialkylaminoalkyl (meth)acrylamides such as dimethylaminoethyl (meth)acrylamide and 3-dimethylamino-2-hydroxypropyl acrylamide!.

The cationic vinyl imidazolines include N-vinyl imidazoline and tertiary and quaternary salts thereof; the pyridines include 2-vinyl pyridine, 3-vinyl pyridine, N-vinyl pyridine, and tertiary and quaternary salts thereof; the vinylbenzyl quaternary ammonium salts include vinylbenzyl tri-C₁₋₄ alkyl ammonium salts such as those disclosed in the specification of British Pat. No. 862,719; and the allylamines include (meth)allylamines (denoting allylamine and methallylamine collectively; which expression will be similarly used hereinafter in the specification) and mono- and di-C₁₋₄ alkyl substitution products thereof, di(meth)allylamines and alkyl substitution products thereof, and quaternized products of these alkyl-substituted (meth)allylamine.

Other ethylenically unsaturated monomer optionally copolymerized with the aforementioned cationic monomer are nonionic monomers such as (meth)acrylamides, N-mono and N,N-di-C₁₋₁₄ alkyl (meth)acrylamides, (meth) acrylonitriles, C₁₋₄ alkyl (meth) acrylates, styrene, vinyl esters (such as vinyl acetate), vinyl ethers (such as vinylmethyl ether), and vinyl halides (such as vinyl chloride) and anionic monomers such as unsaturated carboxylic acids such as (meth)acrylic acids and maleic acid!, unsaturated sulfonic acids such as aliphatic sulfonic acids including vinyl sulfonic acid and (meth)allyl sulfonic acids, aromatic vinyl sulfonic acids including vinyl toluene sulfonic acid and styrene sulfonic acid, sulfo(meth)acrylates including sulfo C₂₋₄ alkyl (meth)acrylates, and 2-hydroxy-3-(meth)acryloxypropane sulfonic acids, and sulfo(meth)acrylamides including (meth)acrylamide C₂₋₄ alkane sulfonic acid and 3-(meth)acrylamide-2-hydroxypropane sulfonic acid and salts thereof, such as alkali metal (Na, K, etc.) salts, ammonium salts, and amine salts including mono-, di-, and tri-ethanolamines and alkyl (C₁₋₄) amines. The proportion of the cationic monomer is generally at least 5%, desirably at least 10%, and particularly desirably at least 30%, based on the weight of all the monomers involved. The proportion of the (meth)acrylamide is generally in the range of 0 to 95%, preferably in the range of 0 to 70%. The proportion of the anionic and hydrophobic monomer is generally not more than 20%, preferably not more than 10%. The polymer and the copolymer of the cationic monomer optionally with some other monomer are found among those disclosed in the U.S. Pat. Nos. 4,152,307 and 3,259,570.

Other examples of the cationic high molecular weight destabilizers are cationically modified polyacrylamides, chitosan, polyethyleneimines, and epihalohydrin-amine condensates and cationized starches. Specific examples of cationically modified polyacrylamides are Mannich modification products (such as disclosed in the specification of U.S. Pat. No. 2,328,901) and Hofmann modification products of polyacrylamides. Examples of the polyethyleneimine are polyethyleneimines of polymerization degrees of 400 or more, preferably 2,000 or more, N-methyl substitution products thereof, and tertiary and quaternary salts of these (such as those disclosed in the specification of U.S. Pat. No. 3,259,570). Specific examples of the epihalohydrin-amine condensates are polycondensates of epichlohydrin with an alkylenediamine of two to six carbon atoms. Specific examples of the cationized starches are cationic starches, disclosed in the Encyclopedia of Chemical Technology (2nd edition), Vol. 18, pp 688-689. Specific examples of the chitosan are products obtained by heating chitins derived from shellfish such as squid, shrimp, etc.

The inorganic or organic cationic material is typically added to the wastewater stream after the stream is collected in a holding or treating tank. An effective amount of the cationic polymer, typically up to about 1500 parts per million based on the total accumulated effluent, is added to the effluent to participate in coagulation, destabilization or removal of the emulsified hydrophobic soils. Preferably the cationic material is added at a concentration of about 100 ppm to 1000 ppm, preferably from about 200 ppm to 800 ppm, based on the total collected effluent.

The Amphoteric Carboxylate

The amphoteric carboxylate is a compound having the following formula: ##STR2## wherein X is a linear or branched alkylene, hydroxyalkylene or alkoxyalkylene group having 1-4 carbon atoms;

R is R⁴ --CO--NH in which R⁴ is a saturated or unsaturated, branched or linear alkyl group having 6-22 carbon atoms, or R⁴ ;

R¹ is hydrogen, A or (A)_(n) --X--CO₂ ⁻ Z⁺ in which A is a linear or branched alkyl, hydroxyalkyl or alkoxyalkyl having 1-4 carbon atoms, n is an integer from 0 to 6, and Z is an alkali metal cation, a hydrogen ion or an ammonium cation;

R² is (A)_(n) --X--CO₂ ⁻ Z⁺ ; and

R³ is absent or A. Particularly valuable materials for use in this invention are the amphoteric dicarboxylate and monocarboxylate materials such as, for example, disodium cocoamphodiacetate, disodium cocoamphodipropionate, disodium cocoaminodipropionate sodium cocamphomonoacetate, cocamidopropyl betaine, alkyl betaine, e.g. cetyl betaine, dihydroxyethyl tallow glycinate, sodium lauriminodipropionate, or mixtures thereof. These materials are available from Mona Industries, Inc., Patterson, N.J. and Rhone-Poulenc, Inc.

The above disclosed amphoteric carboxylate surfactant material can be separately added to the aqueous stream at any point during its creation or treatment. The amphoteric carboxylate can be added in a single portion, can be divided into several portions separately added or can be continuously metered into the aqueous stream. Typically the amphoteric material is added prior to the addition of a cationic destabilizer or flocculent and prior to any pH change or separation initiation. One preferred mode of utilizing the amphoteric carboxylate material in separating hydrophobic soils from an aqueous stream involves using a detergent composition formulated with the amphoteric carboxylate material. Such aqueous detergents can be used in a variety of cleaning protocols including laundry, floor cleaning, equipment cleaning, etc. The detergent composition contains a fully formulated built system using the amphoteric carboxylate as a component of the detergent. The detergent composition can contain a variety of other ingredients including both organic and inorganic functional materials, builders, etc.

Nonionic surfactant materials that can be used in the laundry compositions of the invention comprise either a C₈₋₁₈ alcohol ethoxylate that corresponds to the following formula:

    C.sub.8-18 Alkyl-O-(EO).sub.m --H

wherein the alcohol ethoxylate has 3-15 moles of ethylene oxide, or mono- or di- a C₈₋₁₂ alkyl phenol ethoxylate corresponding to the following formula: ##STR3## wherein p is 1 or 2 and the alkyl groups can be straight or branched chain or can be substituted by a common substituent and the ethoxylate compound can contain 3 to 15 moles of ethylene oxide, preferably 3 to 12 moles of ethylene oxide, most preferably 4 to 9.5 moles of ethylene oxide.

When the separation technology of the invention is used in a laundry composition, it can be combined with an alkaline source. As utilized herein, the term "alkaline source" refers to those alkaline compounds which are known to be useful as builders in detergent compositions for improving soil removal performance. Typical sources of alkalinity include the sodium and potassium hydroxides and the sodium and potassium silicates. Sodium carbonate is also a typical source of alkalinity in detergent compositions. Such sources of alkalinity are commonly available in either aqueous or powdered form which are both generally useable in formulating typical detergent compositions.

A second detergent component useful in a detergent composition is a surfactant. Surfactants are those organic compounds which include both a hydrophilic and a hydrophobic moiety on the same molecule and therefore are able to assist in the performance of a detergent composition by enhancing wetting of the substrate, suspending removed contaminants, and various other functions. A wide selection of anionic and nonionic surfactants providing various combinations of characteristics are commercially available from a number of sources. For a detailed discussion of surfactants see Kirk-Othmer, Encvclopedia of Chemical Technology, Second Edition, volume 19, pages 507-592.

A third detergent component useful in a detergent composition is a chelating/sequestering agent. Generally, chelating agents are those molecules capable of coordinating the metal ions commonly found in natural water and thereby preventing the metal ions from interfering with the functioning of the other detersive component(s) of the composition. Useful chelating agents include aminocarboxylic acids, condensed phosphates and polyacrylates.

Suitable aminocarboxylic acids include specifically, but not exclusively, N-hydroxyethyliminodiacetic acid, nitrilotriacetic acid (NTA), ethylenediaminetetraacetic acid (EDTA), N-hydroxyethyl-ethylenediaminetriacetic acid (HEDTA), and diethylenetriaminepentaacetic acid (DTPA).

Suitable condensed phosphates include specifically, but not exclusively phosphates such as sodium and potassium orthophosphate, sodium and potassium pyrophosphate, sodium tripolyphosphate, and sodium hexametaphosphate.

Suitable polyacrylates include specifically, but not exclusively, polyacrylic acid, polymethacrylic acid, acrylic acid-methacrylic acid copolymers hydrolyzed polymethacrylamide, hydrolyzed polyamide-methacrylamide copolymers, hydrolyzed polyacrylonitrile, hydrolyzed polymethacrylonitrile, and hydrolyzed acrylonitrilemethacrylonitrile copolymers. For a detailed discussion of chelating agents/sequestrants, see Kirk-Othmer, Encyclopedia of Chemical Technology, Second Edition, volume 6, pages 1-24.

Many colored materials contain a conjugated chain (a chain of alternating single and double bonds) with a terminal atom or group of atoms which can resonate between two different covalent states. The color of such materials may be destroyed by breaking one of the double bonds in the conjugated chain and/or chemically modifying the terminal atom or atoms so as to prevent resonation. Hence, any chemical compound capable of chemically breaking a conjugated double bond and/or capable of modifying a resonating atom or group of atoms so as to interfere with resonation may be effective as a bleach.

Broadly, the five categories of bleaching materials include: (i) chlorine, (ii) hypochlorites and chloramines, (iii) hydrogen peroxide and other peroxy compounds, (iv) chlorite and chlorine dioxide, and (v) reducing agents. Generally, the preferred bleaching agent for use in laundry, warewashing and hard surface cleaners are those bleaches capable of liberating an active halogen species, under those conditions normally encountered in the cleansing processes. Based upon superior bleaching performance and ready availability, the preferred halogen releasing compounds typically include the alkali metal dichloroisocyanurates, chlorinated trisodiumphosphate, the alkali metal hypochlorites, monochloramine and dichloramine. Bleaching agents are generally deactivated when placed in an alkaline environment such as found within detergent compositions containing an alkaline source. Accordingly, additional steps may be required to maintain activity of a bleaching agent within a detergent composition. See, for example, U.S. Pat. Nos. 4,657,784 and 4,681,914. For a detailed discussion of bleaching agents, see Kirk-Othmer, Encyclopedia of Chemical Technology, Second Edition, volume 3, pages 550-566.

A fifth detergent component useful in a detergent composition is a defoamant. Typical defoamers are those compounds having a hydrophilic/hydrophobic balance suitable for reducing the stability of foam. The hydrophobicity is typically provided by an oleophilic moiety such as an aromatic alkyl or aralkyl group or an oxypropylene group or chain.

The hydrophilicity is typically provided by an oxyethylene group or chain or an ester group. The most frequently utilized defoamers include the phosphate esters and the nonionic organic surface-active polymers (surfactants) having both a hydrophobic groups or block and a hydrophilic ester-groups or block such as a nonylphenol ethoxylate. A discussion of defoaming nonionic surfactants may be found in U.S. Pat. No. 3,048,548 (Martin et al), U.S. Pat. No. 3,334,147 (Brunelle et al), and U.S. Pat. No. 3,442,242 (Rue et al).

A sixth detergent component useful in a detergent composition is an enzyme effective for catalyzing the break down of various contaminating compounds commonly found on the substrate(s) to be cleaned. Commonly employed enzymes include the proteinases which are capable of catalyzing the hydrolysis of proteinaceous materials, amylases which are capable of catalyzing the hydrolysis of polysaccharides, and lipases which are capable of catalyzing the hydrolysis of fats.

In addition to those components previously described, other conventional detergent components may be incorporated into the detergent composition so long as they do not meaningfully interfere with cleaning or pH initiated phase separation. Such components may include such compounds as bactericides, brightening agents, antiredeposition agents, inorganic salts, dyes and fragrances.

The formulated detergent composition of the invention can correspond with the following proportions set forth in Table I.

                  TABLE I                                                          ______________________________________                                                                           Most                                         Powder         Useful    Preferred                                                                               Preferred                                    ______________________________________                                         Source of Alkalinity                                                                          5-95      60-95    65-90                                        Amphoteric carboxylate                                                                        1-20      2-15     2-10                                         Nonionic       1-25      2-20     4-15                                         Sequestrant    0-40      0-20     2-12                                         ______________________________________                                         Liquid         Useful    Preferred                                                                               Preferred                                    ______________________________________                                         Source of Alkalinity                                                                          5-20      0-10     0-5                                          Amphoteric carboxylate                                                                        2-40      10-35    25-30                                        Nonionic       40-98     50-90    60-75                                        Sequestrant    0-20      4-15     4-10                                         ______________________________________                                    

The laundry compositions of the invention can comprise a number of product formats. The materials can be manufactured as liquid concentrates, particulate solids, pellets, or cast solid materials contained in either a solid plastic container or wrapped in water soluble or insoluble film.

We have found that the hydrophobic soil separation technology of this invention, operates through a cooperative action between the amphoteric carboxylate surfactant and the flocculent (or cationic destabilizer) at low pH to separate the hydrophobic soil from the aqueous stream. The preferred mode of addition of the materials in a laundry effluent separation process involves a first use of a fully formulated laundry detergent material containing the amphoteric carboxylate material. The laundry fabric is cleaned of hydrophobic soil using the fully formulated laundry detergent. The hydrophobic soil containing aqueous effluent passes from the laundry machine into a disposal system. The stream can be processed continually or can be processed semicontinuously or in a batch-wise mode. Since the aqueous laundry effluent contains the amphoteric carboxylate surfactant resulting from the laundry protocol, the stream is first acidified to a pH less than 7 using a sufficient amount of an acidic material to result in the desired pH. Typically, strong organic and inorganic acids can be added. Such acids include hydrochloric acid, nitric acid, phosphoric acid, sulfuric acid, acetic acid, trichloroacetic acid and others. Once the pH of the aqueous stream is adjusted to a preferred acidic pH, the stream is contacted with a source of the flocculent or cationic destabilizer material. In the process, the aqueous stream is contacted with the flocculent for a sufficient period of time to result in a phase separation of the hydrophobic soil that is sufficiently complete to result in a residual concentration of hydrophobic soil that is acceptable for municipal sanitation operation procedures. In a continuous process, the chemicals are metered into the stream to result in an effective concentration of the acidulant and the flocculent. The piping and tanks of the continuous system are sized and configured to ensure appropriate mixing, and sufficient separation time to result in the desired effluent concentration. In a batch process, the effluent stream is directed into a holding tank wherein it is treated with acidulant followed by a flocculent material either in the same tank or in separate treatment tanks. The tanks are suitably agitated and after phase separation, either the aqueous material is taken off the bottom of the tank or the hydrophobic soil is skimmed from the top of the tank. The treated aqueous stream can be directed to the municipal sewer system.

An amount of the amphoteric carboxylate surfactant composition is added to the stream such that the concentration of the amphoteric material reaches an effective pH change separating concentration which is typically less than about 1000 ppm based on the total amount of effluent. Preferably, the surfactant material is used at a concentration of about 10-1000 ppm, most preferably about 100 to about 500 ppm.

Similarly, the composition having sufficient acidity to change the pH of the effluent from approximately neutral or mildly alkaline to a pH less than 7, preferably less than 6, most preferably in the range of from about 3 to about 5.5 is added to the effluent material typically by metering the acidic material into a line leading to the holding or treating tank or into the treating tank directly. The pH of the material in the holding tank or in the line can be monitored to ensure that the acid material is added in sufficient proportions to maintain an effective pH change.

An amount of the flocculent or the cationic destabilizer material is added to the aqueous stream either in a continuous or batch-wise processing mode such that the concentration of the flocculent causes a rapid and substantially complete separation of the hydrophobic soil from the aqueous stream. Typically, an effective amount of the flocculent comprises about 10 to 1250 ppm of the material based on the aqueous stream. Preferably, the flocculent material is added to the aqueous stream at a concentration of about 10 to 1000 ppm, most preferably about 10 to 500 ppm for reasons of economy and rapid aqueous stream processing.

In the practice of the laundry chemical aspect of the invention, the soiled items are laundered in a commercial laundry machine in which the soiled item is contacted with an aqueous cleaning composition containing the ingredients disclosed at use levels of about 0.5 to 10 lbs. of composition per each 100 lbs. of fabric, rag, towel or other soiled unit. Typical laundry cycles are used in laundering the soiled items. After laundering is complete, the effluent contaminated with the hydrophobic organic soils can be accumulated and treated. In the practice of the invention, the effluent is treated after leaving the machine or is accumulated in any convenient storage vessel having appropriate handling equipment for addition of the pH change chemical. Such pH change chemicals can comprise common acidic material capable of changing the pH of the effluent from the pH typically between 8 and 12 to a pH less than 6. Suitable addition controls, agitators, and pH monitoring equipment are desirable. Further, the effluent container could be equipped with a site for removal of a sample for testing. The effluent can be tested for residual hydrophobic soil during phase separation. The effluent container should also be equipped with means to remove the treated effluent to a sewer discharge. Further, the container should be equipped with apparatus that can safely remove the demulsified soils to appropriate disposal.

In our work with the laundry detergent composition of the invention, we have found that the compositions of the invention display superior performance when its pH controlled separation properties are compared to other surfactant systems in terms of residual hydrophobic soil concentration and the pH of the phase break between the hydrophobic portion and the aqueous portion. The compositions of the invention, and the performance of the composition in cleaning and phase separation are exemplified in the following examples and tables. We believe the performance of the separation chemicals in the laundry systems set forth below shows that the chemicals will perform similarly in any generic aqueous waste stream containing hydrophobic soil. The following contains a best mode.

The above discussion, examples and data provide a basis for understanding the disclosure. However, the invention can embody a variety of compositions. The invention accordingly is found in the claims hereinafter appended.

EXAMPLE 1 ##STR4##

The compositions set forth in Table II were evaluated for cleaning capacity and for performance in separating the hydrophobic soil from the aqueous effluent. The evaluations of cleaning performance were based on a powdered laundry detergent based on amphoteric carboxylate-containing surfactant chemistry. The formulas to be evaluated including comparative preparation and Examples 1-5 were evaluated using a common laundry procedure set forth in Table III.

                                      TABLE II                                     __________________________________________________________________________                     COMPARATIVE PREP                COMPOSITIONS I-V               RAW MATERIAL    CONTROL                                                                              COHEN                                                                               MALONEY                                                                              MCFARLAN                                                                              CP1 CP2 CP3 CP4 CP5                    __________________________________________________________________________     NPE 9.5         4.0%                    4.0%                                                                               4.0%                                                                               4.0%                                                                               4.0%                                                                               4.0%                   NPE 4.5         4.0%             9.0%   4.0%                                                                               4.0%                                                                               4.0%                                                                               4.0%                                                                               4.0%                   EP/PO Capped Surfactant - Cohen.sup.1                                                                4.0%                                                     EP/PO Capped Surfactant - Cohen.sup.2                                                                4.0%                                                     Amine Ethoxylate - Maloney.sup.3                                                                          8.0%                                                Octyldipropionate - Cohen.sup.4                                                                      3.0%                                                     Cocoamphomonoacetate.sup.5                              4.0%                   Capryloamphodipropionate.sup.6                      4.0%                       Capryloamphopropionate - McFarlan.sup.7                                                                         2.0%                                          Cocoamphodipropionate.sup.8             8.0%                                                                               4.0%                               Cocoamphodiacetate.sup.9                        4.0%                           Soda Ash Lt. Dens                                                                              23.2% 23.2%                                                                               23.2% 23.2%  19.2%                                                                              23.2%                                                                              23.2%                                                                              23.2%                                                                              23.2%                  Soda Metasilicate                                                                              63.0% 63.00%                                                                              63.0% 63.0%  63.0%                                                                              63.0%                                                                              63.0%                                                                              63.0%                                                                              63.0%                  Amorphorous Silicate Form.sup.10                                                               1.8%  1.8% 1.8%  1.8%   1.8%                                                                               1.8%                                                                               1.8%                                                                               1.8%                                                                               1.8%                   Salt (NaCl)     4.0%  1.0% 4.0%  1.0%                                          TOTAL           100.0%                                                                               100.0%                                                                              100.0%                                                                               100.0% 100.0%                                                                             100.0%                                                                             100.0%                                                                             100.0%                                                                             100.0%                 __________________________________________________________________________      .sup.1 FEP-25                                                                  .sup.2 LFEP-61                                                                 .sup.3 TOMAN ET-5                                                              .sup.4 OPDLF                                                                   .sup.5 ULTRA                                                                   .sup.6 811                                                                     .sup.7 CyNa50                                                                  .sup.8 CEM                                                                     .sup.9 CDX                                                                     .sup.10 Sipernate                                                        

                  TABLE III                                                        ______________________________________                                         Typical Wash Formula Using Alkaline Powder Composition                         OPERATION TEMP (°F.)                                                                         TIME (min) PRODUCT                                        ______________________________________                                         FLUSH     HOT        2                                                         BREAK     170        15         4 lbs. detergent/                                                              100 lbs. fabric                                CARRYOVER 170        5                                                         RINSE     HOT        2                                                         DYE BATH  HOT        6                                                         5 RINSES  HOT/COLD   2 (Each)                                                  ______________________________________                                    

The experimental results summarized in Tables IV and V show the effectiveness of the detergents of the invention and the effectiveness of the separation technology. In Table IV under wash quality, a wick time test is used to demonstrate that the compositions of the invention can be very effective soil removing detergent compositions. In the data called water quality, the ability of the separation technology to result in low residual hydrophobic soil is demonstrated. In the wick time data a rapid time shows excellent cleaning properties. In the water quality data a low number indicates low residual hydrophobic soil content.

                                      TABLE IV                                     __________________________________________________________________________            WASH QUALITY               WATER QUALITY (COMPOSITE SAMPLE)                    WICK TIME             RAW  FOG AFTER 5 MIN.sup.1                                                                    NTU AFTER 5 MIN.sup.2                     1 INCH    2 INCH      WATER                                                                               pH        pH                                        SECONDS                                                                              STD DEV                                                                             SECONDS                                                                              STD DEV                                                                             FOG  4  6   8  4  6   8                           __________________________________________________________________________     CONTROL                                                                               7.8   2.3  32.6  7.7  5800 5400                                                                              6500                                                                               5300                                                                              1280                                                                              1150                                                                               1260                        COHEN  20.9  15.6 50.1  18.8 5800 2000                                                                              3000                                                                               3600                                                                              1280                                                                              1200                                                                               1260                        MALONEY                                                                               47.9  15.8 101.5 27.3 3200 4400                                                                              4300                                                                               3900                                                                              1000                                                                              1100                                                                               1050                        MCFARLAN                                                                              6.9   1.7  31.0  8.6  2100 420                                                                               340 1200                                                                              430                                                                               1140                                                                               1100                        EX1    5.5   1.1  26.0  4.4  2500 290                                                                               2000                                                                               2000                                                                              48 500 520                         EX1 (repeat)                 6100 240                                                                               1900                                                                               5000                                                                              70 365 500                         __________________________________________________________________________      .sup.1 EPA 413.4                                                               .sup.2 EPA 180.1                                                         

                                      TABLE V                                      __________________________________________________________________________     Polymer (ppm).sup.11                                                           CATIONIC A       CATIONIC B  CATIONIC C                                        pH    8  6   4   8   6   4   8   6   4                                         __________________________________________________________________________     CONTROL                                                                              800                                                                               600 600 1500                                                                               1500                                                                               650 2100                                                                               2100                                                                               900                                       CEM2.sup.12                                                                          600                                                                               400 100 1000                                                                               850 350 1500                                                                               1200                                                                               500                                       CEM1.sup.12                                                                          300                                                                               60  40  800 150 50  1100                                                                               175 100                                       CDX.sup.12                                                                           775                                                                               300 50  1600                                                                               700 125 2600                                                                               1100                                                                               200                                       CYN.sup.13                                                                           600                                                                               400 300 1300                                                                               700 500 1800                                                                               700 600                                       __________________________________________________________________________      .sup.11 Minimum concentration of cationic polymer needed to demulsify and      separate hydrophobic soil                                                      .sup.12 Uses amphoteric dicarboxylate chemistry                                .sup.13 McFarlan patent chemistry                                        

The wick time test is a qualitative test used to predict cleaning properties in fabric cleaned with the test formula. In the wick time test, a red shop towel (approximately 12 inches×12 inches) is immersed in a tray or pan containing 1-2 inches of water. The towel is hung on a bar or line and immersed in the water, held in place using a bar or other weighting system. The time taken by the water to reach a one inch level or a two inch level is measured. The ability of the water to wet the fabric is characteristic of a high quality cleaning detergent used to clean the fabric. A fabric soiled by residual oil or fat will wick more slowly than a clean fabric. Accordingly, the rapidity with which the aqueous material wets and ascends the shop towel through the fabric mesh qualitatively characterizes the likely detergent properties of the detergent.

The data in the water quality portion of Table IV is obtained using EPA method 413.4 to obtain the fats, oils and grease content (FOG) after five minutes of separation time after the addition of the cationic or flocculent material. The data labeled NTU is obtained using EPA procedure 180.1 after five minutes of separation.

Inspecting the data set forth in Tables IV and V, the performance of all compositions of the invention substantially improved over the comparative preparations of the standard commercial prior art material. In particular, the material identified as Composition (CP1) containing a preferred amphoteric carboxylate has clearly superior performance.

EXAMPLE 2

The compositions set forth in Table VI using a common laundry procedure set forth in Table VI were evaluated to determine the amount of cationic destabilizer in parts per million required to break the emulsion as compared to the control where the standard is the amount of nonionic surfactant required, Table VII.

                                      TABLE VI                                     __________________________________________________________________________     WASH PARAMETERS                                                                                       OZ/CWT                                                  OPERATION                                                                             TEMP                                                                               TIME                                                                               PRODUCT I II III                                                                               IV V                                            __________________________________________________________________________     Flush  160 2:00                                                                               --                                                              Break  180 15:00                                                                              Silicate of Soda                                                                       64                                                                               64 64 64 64                                                          Caustic soln.                                                                          24                                                                               24 24 24 24                                                          Nonionic                                                                               12                                                                               9  6.2                                                                               9.6                                                                               7.0                                                         Amphoteric                                                                             --                                                                               6  4.1                                                                               4.8                                                                               3.5                                          2 Flushes                                                                             180 1:00                                                                               --                                                              Suds   180 8:00                                                                               Silicate of Soda                                                                       22                                                                               22 22 22 22                                                          Caustic Soda                                                                           10                                                                               10 10 10 10                                                          Nonionic                                                                                6                                                                               4.5                                                                               6.2                                                                               4.8                                                                               3.5                                                         Amphoteric                                                                             --                                                                               3  4.1                                                                               2.4                                                                               1.8                                          Rinses 120 2:00                                                                               --                                                              3 Rinses                                                                              80  2:00                                                                               --                                                              __________________________________________________________________________

                                      TABLE VII                                    __________________________________________________________________________     ppm CATIONIC A.sup.1              ppm CATIONIC B.sup.1                         pH    8% red'n.sup.2                                                                      6% red'n2.sup.                                                                       4% red'n.sup.2                                                                       8% red'n.sup.2                                                                      6% red'n.sup.2                                                                       4% red'n.sup.2                               __________________________________________________________________________     Nonionic.sup.3                                                                       400                                                                               0 380                                                                                5 .sup. ***.sup.4                                                                   N/A                                                                               400                                                                               0 ***                                                                               N/A                                                                               ***  N/A                                     BET-W II.sup.5                                                                       275                                                                               31                                                                               150                                                                               63 ***                                                                               N/A                                                                               275                                                                               31                                                                               175                                                                               56 65   84                                      ULTRA II                                                                             300                                                                               25                                                                               160                                                                               60 50 88 350                                                                               13                                                                               135                                                                               66 50   88                                      CEM II                                                                               200                                                                               50                                                                               120                                                                               70 100                                                                               75 200                                                                               50                                                                               120                                                                               70 70   83                                      CEM III                                                                              350                                                                               13                                                                               200                                                                               50 88 78 350                                                                               13                                                                               160                                                                               60 40   90                                      CEM IV                                                                               225                                                                               44                                                                               150                                                                               63 50 88 250                                                                               38                                                                               113                                                                               72 40   90                                      CLV II                                                                               400                                                                               0 230                                                                               41 113                                                                               72 450                                                                               0 200                                                                               50 113  72                                      CLV III                                                                              400                                                                               0 350                                                                               13 ***                                                                               N/A                                                                               400                                                                               0 300                                                                               25 ***  N/A                                     TM II 300                                                                               25                                                                               ***                                                                               N/A                                                                               ***                                                                               N/A                                                                               200                                                                               50                                                                               ***                                                                               N/A                                                                               ***  N/A                                     H2C-HA II                                                                            400                                                                               0 300                                                                               25 ***                                                                               N/A                                                                               400                                                                               0 300                                                                               25 200  50                                      __________________________________________________________________________      .sup.1 Cationic A is a quaternary ammonium polymer, Cationic B is a            polyquaternary amine.                                                          .sup.2 % red'n is the reduced percentage of polymer required to demulsify      and separate the hydrophobic soil as compared to the controlnonionic stud      at pH = 8 (line 1).                                                            .sup.3 Nonionic is the control study without amphoteric surfactants, i.e.      only nonionic surfactant and polymer.                                          .sup.4 *** represents no demulsifying found in system.                         .sup.5 BETW II is an example of using Mirataine BETW, under wash conditio      II from Table VI. The other studies listed use the same terminology.      

We claim:
 1. An alkaline cleaning concentrate composition comprising in powder form:(a) an effective detergent amount comprising 5 to 95 wt-% of a source of alkalinity; (b) an effective detergent and pH phase separation amount comprising about 1-20 wt-% of an amphoteric carboxylate surfactant of the formula: ##STR5## wherein X is a linear or branched alkylene, hydroxyalkylene or alkoxyalkylene group having 1-4 carbon atoms;R is R⁴ --CO--NH in which R⁴ is a saturated or unsaturated, branched or linear alkyl group having 11-22 carbon atoms, or R⁴ ; R¹ is hydrogen, A or (A)_(n) --X--CO₂ ⁻ Z⁺ in which A is a linear or branched alkyl, hydroxyalkyl or alkoxyalkyl having 1-4 carbon atoms, n is an integer from Q to 6, and Z is an alkali metal cation, a hydrogen ion or an ammonium cation; R² is (A)_(n) --X--CO₂ ⁻ Z⁺ ; and R³ is absent or A; (c) an effective detergent amount comprising about 1 to 25 wt-% of a nonionic surfactant composition comprising a C₈₋₁₂ alcohol ethoxylate of the formula:

    C.sub.8-18 Alkyl-O-(EO).sub.m --H

or a mono- or di-C₈₋₁₂ alkyl phenol ethoxylate surfactant of the formula: ##STR6## each having from 3-15 moles of ethylene oxide per mole of surfactant and p is 1 or 2;wherein when fabric soiled with greasy or oil soils is cleaned in an aqueous cleaning composition containing an effective cleaning amount of the concentrate resulting in an alkaline effluent containing substantial quantities of organic hydrophobic soil which may be separated from the aqueous effluent by contacting the effluent, at a pH less than 7, with an effective amount of cationic emulsion destabilizing composition.
 2. The composition of claim 11 wherein the source of alkalinity comprises a member selected from the group consisting of an alkali metal carbonate, a water soluble alkali metal silicate and mixtures thereof.
 3. The composition of claim 1 which additionally comprises a sequestrant.
 4. The composition of claim 3 wherein the sequestrant comprises sodium tripolyphosphate, sodium pyrophosphate or mixtures thereof.
 5. The composition of claim 3 wherein the organic sequestrant comprises ethylene diamine tetraacetic acid or its sodium salt, nitrilotriaacetic acid or its sodium salt, polyacrylic acid or an acrylic acid copolymer or its sodium salt, or mixtures thereof.
 6. The composition of claims 1 wherein in the amphoteric surfactant R is R⁴ or R⁴ --CO--NH in which R⁴ is a C₁₁₋₁₇ alkyl, X is a linear alkylene group having 1-3 carbon atoms, n is 0-3 and Z is an alkali metal or ammonium cation.
 7. The composition of claim 1 wherein the source of alkalinity comprises a mixture of 5-60 wt-%. of sodium carbonate and 10-70 wt-% of sodium metasilicate.
 8. The composition of claim 1 wherein the source of alkalinity comprises a mixture of 5-60 wt-% sodium carbonate, 20-35 wt-% of sodium hydroxide and 10-70 wt-% of sodium metasilicate, each based on the weight of the total composition.
 9. An alkaline cleaning concentrate composition comprising in powder form:(a) an effective detergent amount comprising 60-95 wt-% of a source of alkalinity; (b) an effective detergent and pH phase separation amount comprising about 2-15 wt-% of an amphoteric carboxylate surfactant of the formula: ##STR7## wherein X is a linear or branched alkylene, hydroxyalkylene or alkoxyalkylene group having 1-4 carbon atoms;R is R⁴ --CO--NH in which R⁴ is a saturated or unsaturated, branched or linear alkyl group having 11-22 carbon atoms, or R⁴ ; R¹ is hydrogen, A or (A)_(n) --X--CO₂ ⁻ Z⁺ in which A is a linear or branched alkyl, hydroxyalkyl or alkoxyalkyl having 1-4 carbon atoms, n is an integer from 0 to 6, and Z is an alkali metal cation, a hydrogen ion or an ammonium cation; R² is (A)_(n) --X--CO₂ ⁻ Z⁺ ; and R³ is absent or A; (c) an effective detergent amount comprising about 2 to 15 wt-% of a nonionic surfactant composition comprising a C₈₋₁₂ alcohol ethoxylate of the formula:

    C.sub.8-18 Alkyl-O-(EO).sub.m --H

or a mono- or di-C₈₋₁₂ alkyl phenol ethoxylate surfactant of the formula: ##STR8## each having from 3-15 moles of ethylene oxide per mole of surfactant and p is 1 or 2; wherein when fabric soiled with greasy or oil soils is cleaned in an aqueous cleaning composition containing an effective cleaning amount of the concentrate resulting in an alkaline effluent containing substantial quantities of organic hydrophobic soil which may be separated from the aqueous effluent by contacting the effluent, at a pH less than 7, with an effective amount of cationic emulsion destabilizing composition.
 10. An alkaline cleaning concentrate composition comprising in powder form:(a) an effective detergent amount comprising 5 to 95 wt-% of a source of alkalinity; (b) an effective detergent and pH phase separation amount comprising about 1-20 wt-% of an amphoteric carboxylate surfactant of the formula: ##STR9## wherein X is a linear or branched alkylene, hydroxyalkylene or alkoxyalkylene group having 1-4 carbon atoms;R is R⁴ --CO--NH in which R⁴ is a saturated or unsaturated, branched or linear alkyl group having 11-22 carbon atoms, or R⁴ ; R¹ is, A or (A)_(n) --X--CO₂ ⁻ Z⁺ in which A is a linear or branched alkyl, hydroxyalkyl or alkoxyalkyl having 1-4 carbon atoms, n is an integer from 0 to 6, and Z is an alkali metal cation, a hydrogen ion or an ammonium cation; R² is (A)_(n) --X--CO₂ ⁻ Z⁺ ; and (c) an effective detergent amount comprising about 1 to 25 wt-% of a nonionic surfactant composition comprising a C₈₋₁₂ alcohol ethoxylate of the formula:

    C.sub.8-18 Alkyl-O-(EO).sub.m --H

or a mono- or di-C₈₋₁₂ alkyl phenol ethoxylate surfactant of the formula: ##STR10## each having from 3-15 moles of ethylene oxide per mole of surfactant and p is 1 or 2;wherein when fabric soiled with greasy or oil soils is cleaned in an aqueous cleaning composition containing an effective cleaning amount of the concentrate resulting in an alkaline effluent containing substantial quantities of organic hydrophobic soil which may be separated from the aqueous effluent by contacting the effluent, at a pH less than 7, with an effective amount of cationic emulsion destabilizing composition.
 11. A cleaning concentrate composition comprising in liquid form:(a) about 0-20 wt-% of a source of alkalinity; (b) about 2-40 wt-% of an amphoteric carboxylic surfactant of the formula: ##STR11## wherein X is a linear or branched alkylene, hydroxyalkylene or alkoxyalkylene group having 1-4 carbon atoms;R is R⁴ --CO--NH in which R⁴ is a saturated or unsaturated, branched or linear alkyl group having 11-22 carbon atoms, or R⁴ ; R¹ is hydrogen, A or (A)_(n) --X--CO₂ ⁻ Z⁺ in which A is a linear or branched alkyl, hydroxyalkyl or alkoxyalkyl having 1-4 carbon atoms, n is an integer from 0 to 6, and Z is an alkali metal cation, a hydrogen ion or an ammonium cation; R² is (A)_(n) --X--CO₂ ⁻ Z⁺ ; and R³ is absent or A; (c) about 40-98 wt-% of a nonionic surfactant composition comprising a C₈₋₁₂ alcohol ethoxylate of the formula:

    C.sub.8-18 Alkyl-O-(EO).sub.m --H

or a mono- or di-C₈₋₁₂ alkyl phenol ethoxylate surfactant of the formula: ##STR12## each having from 3-15 moles of ethylene oxide per mole of surfactant and p is 1 or 2;wherein when fabric soiled with greasy or oil soils is cleaned in an aqueous cleaning composition containing an effective cleaning amount of the concentrate resulting in an alkaline effluent containing substantial quantities of organic hydrophobic soil which may be separated from the aqueous effluent by contacting the effluent, at a pH less than 7, with an effective amount of cationic emulsion destabilizing composition.
 12. The composition of claim 11 wherein the source of alkalinity is selected from the group consisting of an alkali metal carbonate, an alkali metalhydroxide and a water soluble alkali metal silicate and mixtures thereof.
 13. The composition of claim 11 which additionally comprises a sequestrant.
 14. The composition of claim 11 wherein the sequestrant comprises sodium tripolyphosphate, sodium pyrophosphate or mixtures thereof.
 15. The composition of claim 11 wherein the organic sequestrant comprises ethylene diamine tetraacetic acid or its sodium salt, nitrilotriaacetic acid or its sodium salt, polyacrylic acid or an acrylic acid copolymer or its sodium salt, or mixtures thereof. 